• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1996.10b
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• pp.167-170
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• 1996

석탄의 고압 유동층연소는 기존의 PC 보일러보다는 저온 연소로써 NOx의 발생이 억제되며 탈황제를 동시에 주입하여 SOx 발생을 줄일 수 있는 것이 큰 잇점으로서 석탄 신에너지 개발에 유력한 시스템이다. 본 시스템에서 집진은 연소가스 중의 입자가 고온고압에서 고속으로 터빈에서 충돌될 때 일어나는 터빈의 마모, 침식, 및 부식 등을 방지하기 위하여 필수적이다. PFBC 연소기에서 연소된 가스가 정제후에 바로 가스터빈에 주입되기 때문에 PFBC의 집진은 매우 가혹한 조건이다. 뿐만 아니라 차세대에 더욱 높은 열효율 향상과 가스터빈의 수명 연장을 위하여 집진조건이 더욱 가혹해지고 엄격해질 전망이다. 그 동안 PFBC 집진의 연구가 다방면으로 진행되고 있으나 상용화를 위한 준비가 아직 갖추어지지 않았으며 모든 집진 시스템이 잠정적인 문제점을 갖고 있다. 그 중에서도 세라믹 캔들 필터는 성능이 우수하고 가장 많은 운전경험을 갖고 있기 때문에 가장 가까운 시기에 상용화에 성공할 수 있는 집진 시스템이다. 본 고에서는 세라믹 캔들필터 개발의 현황과 핵심 개발과제에 대하여 논의코자 했다.

• Proceedings of the Materials Research Society of Korea Conference
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• 2003.11a
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• pp.50-50
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• 2003

용사 공정은 소재의 표면 특성을 개질하기 위한 가장 효과적인 공정의 하나로서, 최근 항공기용 엔진 부품을 포함하여 자동차, 및 각종 산업 분야에 폭 넓게 사용되고 있으나, 산업 환경의 고도화로 용사 코팅층의 다양한 분야에서의 고특성화가 요구되고 있다. 소재의 나노화는 이러 한 소재의 고 특성화 요구에 부응할 수 있는 새로운 기술로서, 현재 많은 분야에서 응용이 진행되고 있다. 특히 최근에는 나노기술을 용사 공정에 응용하기 위한 시도가 진행되고 있으나, 나노 분말 제조 기술이 아직 확립되어 있지 않고, 또한 나노 분말을 용사 공정에 응용하기 위한 기술의 부족으로 나노 용사공정에의 적용은 제한을 받고 있다. 이를 위해서는 나노분말 제조 기술의 개발이 이루어져야하고, 나노 분말 제조 기술과 용사 분말 제조 기술 그리고 용사 기술의 접목이 이루어 져야하는 어려움이 있다. 본 연구에서는 나노 용사용 분말을 제조하기 위 한 원료용 나노 분말을 화학적 공정에 의하여 제조 한 후, 이 분말의 유동도 및 밀도 제어를 위한 후 처리 공정을 개발하였다. 제조된 분말의 입자 크기는 약 150nm였으며, 용사 분말 제조후 분말의 겉보기 겉보기 밀도가 3.8g/cc로서 일반 용사용 분말에 비하여 우수하였다.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.28 no.1
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• pp.89-98
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• 2004

In this paper, we develope a dispersion model based on the Generalized Langevin Model. Thomson's well-mixed condition is the well known criterion to determine particle dispersion. But, it has 'non-uniqueness problem'. To resolve this, we adopt a turbulent model which is a new approach in this field of study. Our model was greatly simplified under the self-similarity condition, leaving model only two model constants $C_{0}$ and ${\gamma}$$_{5}$ that control the dispersion and spin which measures rotational property of the Lagrangian particle trajectory. We investigated the sign of spin as well as magnitude by using the Direct Numerical Simulation. Model calculations were performed on the neutrally stable boundary layer flow. We found that spin has weak effect on the particle dispersion but it shows the significant effect on the horizontal flux compared to the zero-spin model.

• Journal of the Korean Society of Visualization
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• v.8 no.1
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• pp.13-18
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• 2010

An experimental investigation of the flow around a vertical fence was carried out using a PIV velocity field measurement technique. The vertical fence was embedded in a turbulent boundary layer. The instantaneous velocity fields measured at cross-sectional planes reveal complex longitudinal vortices that vary in size and strength, developing from the upstream location. In the instantaneous vorticity and velocity field data, the shear flow separated from the fence top is highly turbulent and shows unsteady flow characteristics. The topography of the ensemble averaged velocity fields, especially the separation bubble formed behind the fence, shows that the spatial distributions of streamwise velocity (U) and vertical (V) are symmetric, the spanwise velocity (W) is skew-symmetric with respect to the central xy-plane(z=0).

• Korean Journal of Air-Conditioning and Refrigeration Engineering
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• v.7 no.3
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• pp.359-365
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• 1995

The drag reduction phenomenon with an additives of surfactant(STAC, stearlytrimethyl ammonium chloride) and polymer(PEO, polyethlene oxide) was investigated in fully developed turbulent pipe and channel flows at various low Reynolds numbers as well as very low additives concentration. A maximum of 70% drag reduction compared with plain water flow was found. This maximum drag reduction percentage obtained with surfactant solution was slightly higher than that of the Virk's asymptote in polymer solution.

• Journal of the Korean Society of Safety
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• v.13 no.3
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• pp.112-118
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• 1998

This work has been carried out to study the mixing characteristics of solid in vibrating feeder for stable operations of fluidized bed combustion. The system consisted of two particles such that fine particles were located on the top of the coarse particles before vibratory mixing had started. Effect of particle size, particle densities, vibration amplitude and vibration frequency were experimentally obtained. Also, a diffusion model was applied in interpreting the experimental results. From these results, the following empirical equation for the diffusivity was obtained. $0.87{(\frac{d_c}{d_f})}^{0.73}\;{(\frac{\rho_f}{\rho_c})}^{0.53}(A^2f)$.

• Membrane Journal
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• v.28 no.4
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• pp.252-259
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• 2018

An acidic, real metal-plating wastewater was treated by a fluidized bed membrane reactor introduced with granular activated carbon (GAC) as fluidized media. With GAC fluidization, there was no increase in suction pressure with time at each flux set-point applied. At neutral solution pH, much less fouling rate was observed than acidic pH under GAC fluidization. Higher solution pH resulted in the increase in particle size in metal-finishing wastewater, thus producing a less dense cake structure on membrane. More than 95% of chemical oxygen demand was observed from the fluidized bed membrane reactor under GAC fluidization. Total suspended solid concentration in membrane permeate was near zero. At the raw wastewater pH, no removal of copper and chromium by the fluidized bed membrane reactor was observed. As the pH was increased to 7.0, removal efficiency of copper and chromium was increased considerably to 99 and 94%, respectively. Regardless of solution pH tested, more than 95% of cyanide was removed possibly due to the strong adsorption of organic-cyanide complex on GAC in fluidized bed membrane reactor.

• Korean Chemical Engineering Research
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• v.53 no.3
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• pp.333-338
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• 2015

In this study, we investigated carbonation-regeneration and agglomeration characteristics of dry sorbents. Experiment has been proceeded in the batch-type reactor, which is made of quartz: 0.05 m of I.D and 0.8 m in height. The sorbents that is collected at the cyclone of the carbonation reactor of continuous process were used in this study. The reactivity was studied at the various concentrations of water vapor, $N_2$ and $CO_2$ in the fluidizing gas at regeneration reaction. As a result, the reactivity increased as the regeneration temperature increased, the reactivity decreased as the concentration of water vapor increased. The absorption capacity showed the highest value in case of using $N_2$ 100% as regeneration gas. And decreased in order of $H_2O+N_2$, $CO_2$ 100% and $H_2O+CO_2$. The agglomeration characteristics were investigated according to the particle sizes and concentrations of water vapor at carbonation reaction. As a result, the particle with smaller size and higher concentration of water vapor showed the higher agglomeration characteristic.

• Journal of the Korean Recycled Construction Resources Institute
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• v.8 no.3
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• pp.255-262
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• 2020

Blended cement with fly ash and bottom ash from Circulating Fluidized Bed Combustor boiler(CFBC) burned at a low temperature, can be high heat of hydration and abnormal setting caused by higher volumn contents of Fe₂O₃, free-CaO, SO₃. In this study, the ground CFBC bottom ash powder mixed with blast furnace slag was used as substitute activator of gypsum and recycled iron slag was produced from mix and pulverized by ball mill to increase the recycling rate. The effect on compressive strength of cements with the mixture of original and hydrated bottom ash mixtures with BFS with small water, respectively, was analyzed, and it was found that the hydrated bottom ash activator was more effective in initial strength development. To improve the initial strength of blended cement, an activator mixed with a blast furnace slag and bottom ash mixing ratio of 5:95 and 10:90, respectively, the slag cement by about 6%, and it was analyzed to develop an initial strength similar to gypsum as a conventional activator.

• Korean Chemical Engineering Research
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• v.50 no.3
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• pp.516-521
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• 2012

This study developed a simple model to investigate effects of important operating parameters on performance of a bubbling-bed adsorber and regenerator system collecting $CO_2$ from flue gas. The chemical reaction rate was used with mean particles residence time of a reactor to determine the extent of conversion in both adsorber and regenerator reactors. Effects of process parameters - temperature, gas velocity, solid circulation rate, moisture content of feed gas - on $CO_2$ capture efficiency were investigated in a laboratory scale process. The $CO_2$ capture efficiency decreased with increasing temperature or gas velocity of the adsorber. However, it increased with increasing the moisture content of the flue gas or the regenerator temperature. The calculated $CO_2$ capture efficiency agreed to the measured value reasonably well. However the present model did not agree well to the effect of the solid circulation rate on $CO_2$ capture efficiency. Better understanding on contact efficiency between gas and particles was needed to interpret the effect properly.